CN201454430U - Novel air agitation foaming device - Google Patents
Novel air agitation foaming device Download PDFInfo
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- CN201454430U CN201454430U CN2009200969556U CN200920096955U CN201454430U CN 201454430 U CN201454430 U CN 201454430U CN 2009200969556 U CN2009200969556 U CN 2009200969556U CN 200920096955 U CN200920096955 U CN 200920096955U CN 201454430 U CN201454430 U CN 201454430U
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- pipeline
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- mixing apparatus
- metering device
- aerated stirring
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Abstract
The utility model relates to a novel air agitation foaming device consisting of an air intake device, a feeding device and an agitator, wherein the air intake device consisting of an air transmission pipeline, a pressure regulating filtering device and a voltage regulating and current stabilizing metering device. One end of the air transmission pipeline is connected to compressed air, and the air transmission pipeline is provided with the pressure regulating filtering device, the outlet of pressure regulating filtering device is connected with the voltage regulating and current stabilizing metering device. The outlet of the voltage regulating and current stabilizing metering device is connected with the air inlet of a premixing device through a check valve; the discharge hole of the feeding device is connected with the slurry inlet of the premixing device, and the mixture outlet of the premixing device is connected with the feed inlet of the agitating device. The agitating device is a pipeline type high-shearing mixing emulsification device. The utility model has the advantages of scientific and reasonable structure design, accurate control of foaming volume ratio of slurry, even and exquisite foaming effect, easy manufacturing, low cost, low energy consumption, high degree of automation, simple operation, stable running, long service life and the like.
Description
Technical field
The utility model belongs to the foam device field, particularly a kind of aerated stirring foam device.
Background technology
At present, in all conglomeraties, all need use foam device.For example, in food industry, in the production of bread, cake, dessert, biscuit, dairy produce, candy, usually need to adopt foam device, to increase the soft crunchy sensation of food with the processing of foaming of some raw material; In leather is produced, in the technology that leather surface is covered with paint, lacquer, colour wash, etc., also coating need be foamed usually, carry out foamed and sprayed or roller coat, hide the leather surface permanent disability, to improve surface quality, improve leather hand feeling, conservation reduces cost simultaneously; At packaging industry and timber multi-layer sheet production field, often adopt the water-based glue, multilayer material is carried out compound, as adopting foam device, not only can save glue, saving oven dry expense that can also be a large amount of; In Non-Woven Fabric Industry, need carry out the back arrangement to the material of producing, adopt foam device can save finishing agent and oven dry expense equally, and make non-weaving cloth obtain better feel and specific function; In dry method paper industry, adopt the glue of foaming that the processing of reduction dust is done on its surface, can make dry method paper obtain the effect of dried fastness to wet rubbing and fluffy softness, obtain considerable economic.
Existing foam device adopts the cylinder agitating device of built-in impeller mostly, and it can only realize mixed function.Also there is the feed entrance point on agitating device to feed compressed air, to reach the purpose that stirs simultaneously and foam.But it is relatively poor that above-mentioned foam device exists compressed air and slurry to mix degree, and problem such as the foaming ratio is wayward influences product quality.And this kind foam device such as need obtain more fine and smooth foaming effect, then must improve motor speed, the agitating device impeller is rotated at a high speed, thereby the portion of carrying out increase the load of foam device motor, and power consumption is high.Also there are many defectives such as manufacture difficulty is big, cost is high, easily break down, service life is short in addition.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, a kind of reasonable in design is provided, is easy to accurately control the aerated stirring foam device of foaming ratio, uniform in foaming exquisiteness.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of aerated stirring foam device, constitute by inlet duct, feed arrangement and agitating device, it is characterized in that: described inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device, one end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, and the outlet of voltage stabilization and current stabilization metering device connects the gas feed of a pre-mixing apparatus by a non-return valve; The discharging opening of described feed arrangement is connected with the slurry import of pre-mixing apparatus, and the compound outlet of pre-mixing apparatus is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.
And described feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter.
And, gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, gas transfer pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, this two pressure sensor all is connected with the signal input part of a controller, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.
And described frequency converter is connected with controller.
And the stratiform stainless steel porous plate filler that described pre-mixing apparatus is radially installed by tubular shell and inner institute constitutes, and is shaped on gas feed and slurry import at an end of tubular shell, is shaped on compound at the other end of tubular shell and exports.
And, between single-screw (single screw) pump and pre-mixing apparatus, be connected the clean water pipeline by valve.
And, be connected and installed the pulp pipeline at the grout outlet of high shear mixing emulsifier unit, a magnetic valve is installed on the pulp pipeline, this magnetic valve is controlled by a time relay.
And, in the end of pulp pipeline the sizing head being installed, this sizing head is installed on the slide, and this slide is movably installed on the guide rail, and slide is moved back and forth along guide rail by drive mechanism.
And, two sizing heads are installed on described pulp pipeline, this two sizings head symmetry is installed on separately on the slide, and its slide is movably installed in respectively on the guide rail, and two slides all move back and forth along guide rail separately synchronously by drive mechanism.
Advantage of the present utility model and beneficial effect are:
1. this aerated stirring foam device adopts pipeline high shear mixing emulsifier unit that mixed slurry is carried out the high speed shear stirring, can effectively improve the foaming effect of slurry, the foaming that makes slurry is uniform and smooth more, and energy consumption is low, stable, long service life.
2. the control of passing through voltage stabilization and current stabilization metering device and frequency converter of this aerated stirring foam device can realize the accurate control to admission pressure and inlet amount, thereby the control foam volume is than accurate more, stable.
3. the compressed air and the slurry of this aerated stirring foam device enter pre-mixing apparatus jointly, and in pre-mixing apparatus, fully mix under the effect of set stratiform stainless steel porous plate filler, more existing jet blower more can make liquid fully mix with gas reliably, also can guarantee the continous-stable discharging simultaneously.
4. be connected the clean water pipeline by valve between the single-screw (single screw) pump of this aerated stirring foam device and the pre-mixing apparatus; after foaming is finished and is shut down; adopt purging system that single-screw (single screw) pump, pre-mixing apparatus and pipeline high shear mixing emulsifier unit are cleaned; remain in device inside with slurry-free, influence operate as normal.
5. the pulp pipeline installed of this aerated stirring foam device high shear mixing emulsifier unit is provided with magnetic valve, and by the unlatching and the shut-in time of time relay control magnetic valve, its purpose is to control the time of slurry in high shear mixing emulsifier unit internal stops, makes slurry fine and smooth more, even.
6. this aerated stirring foam device is equipped with the sizing head on the pulp pipeline that the high shear mixing emulsifier unit is installed, the sizing head is moved back and forth along guide rail by drive mechanism, because the flowability of the slurry after this inflating and stirring device of process is handled reduces, therefore, sizing head by the activity setting can be coated slurry the whole breadth of pending product more uniformly, and, can adopt the mode that is symmetrical arranged the sizing head to carry out synchronous pasting and handle as needing double spread.
7. the utility model scientific structure design is reasonable, can accurately control the foam volume ratio of slurry, the foaming effect uniform and smooth, have simultaneously be easy to manufacture, advantages such as cost is low, energy consumption is little, automaticity is high, simple to operate, stable, long service life.
Description of drawings
Fig. 1 is an operation principle schematic diagram of the present utility model;
Fig. 2 is the structural representation (partly cuing open figure) of pre-mixing apparatus of the present utility model;
Fig. 3 is the structural representation (being installed on the roller coating device top) of the utility model sizing head;
Fig. 4 is the vertical view of Fig. 3.
The specific embodiment
The utility model is described in further detail below by specific embodiment, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
A kind of aerated stirring foam device is made of inlet duct, feed arrangement and agitating device, and its innovation part is: inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device.One end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, make the air pressure of being measured more accurate, course of conveying is more stable, be not subjected to the influence of pipeline compressed air pressure in early stage, the outlet of voltage stabilization and current stabilization metering device connects the gas feed of pre-mixing apparatus by a non-return valve.
Feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter, and the discharging opening of single-screw (single screw) pump is connected with the slurry import of pre-mixing apparatus.
As shown in Figure 2, pre-mixing apparatus is made of tubular shell 2 and the inner stratiform stainless steel porous plate filler of being installed 3, end at tubular shell is shaped on gas feed 4 and slurry import 5, be shaped on the outlet 1 of compound at the other end of tubular shell, the compound outlet is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.Be connected the clean water pipeline by valve between single-screw (single screw) pump and pre-mixing apparatus, the water inlet of clean water pipeline feeds cleaning water.
The stirring-head of pipeline high shear mixing emulsifier unit is formed by a plurality of separate chamber polyphones that are made of rotor stator, gas-liquid mixture moves to the process of another chamber from a chamber, obtain sufficient shear action, make two phase flow fully be mixed into a phase, realize the refinement of gas-liquid mixture, make the foam of the foaming slurry that is obtained evenly fine and smooth more.Because stirring-head can be organized polyphone more and use, so it has the advantage that cost is low, reliability is good, in addition, owing to adopt associated mode between each stirring-head and the drive motors, does not need its speed is regulated, make and operation more simple and easy to do.At pipeline high shear mixing emulsifier unit outer setting cooling system, this cooling system can be for being arranged on the water jacket of emulsifier unit outside, and water jacket is connected with cooling water pipeline, and the water inlet of cooling water pipeline feeds cooling water.Thereby can reduce the operating temperature of device, the job stability of holdout device integral body.
Gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, the signal input part of this two pressure sensors homogeneous controller connects, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.The signal output part of this controller also links to each other with frequency converter.By control, can make more accurate, the more stable metering of desired compression air acquisition in the course of work to the voltage stabilization and current stabilization metering device; Regulate the single-screw (single screw) pump rotating speed by frequency converter, realizing metering and pressure control to slurry, thereby the control foam volume than more accurately, stable.Have the automaticity height, simple to operate, the advantage that is easy to control.
Grout outlet at the high shear mixing emulsifier unit is connected and installed the pulp pipeline, and a magnetic valve is installed on the pulp pipeline, and this magnetic valve is controlled by a time relay.By the unlatching and the shut-in time of time relay control magnetic valve, its purpose is to prolong the time of slurry in high shear mixing emulsifier unit internal stops, makes slurry fine and smooth more, even.
Operation principle of the present utility model is:
Compressed air at first enters the pressure regulation filter, obtain to enter the voltage stabilization and current stabilization metering device behind the system works pressure, compressed air is accurately entering pre-mixing apparatus inside behind control flow and the pressure, through pre-mixing apparatus compressed air and slurry are fully mixed, enter high shear mixing emulsifier unit inside then and carry out high-speed stirred, thus finish the foaming slurry the foam thinning process.The foaming slurry is evenly coated product surface by the sizing head of activity setting.After foaming is finished and shut down, adopt purging system that single-screw (single screw) pump, pre-mixing apparatus and pipeline high shear mixing emulsifier unit are cleaned.
Claims (9)
1. aerated stirring foam device, constitute by inlet duct, feed arrangement and agitating device, it is characterized in that: described inlet duct is made of gas transfer pipeline, pressure regulation filter, voltage stabilization and current stabilization metering device, one end of gas transfer pipeline connects compressed air, the pressure regulation filter is installed on the gas transfer pipeline, the outlet of pressure regulation filter connects the voltage stabilization and current stabilization metering device, and the outlet of voltage stabilization and current stabilization metering device connects the gas feed of a pre-mixing apparatus by a non-return valve; The discharging opening of described feed arrangement is connected with the slurry import of pre-mixing apparatus, and the compound outlet of pre-mixing apparatus is connected with the charging aperture of agitating device, and this agitating device is a pipeline high shear mixing emulsifier unit.
2. aerated stirring foam device according to claim 1 is characterized in that: described feed arrangement is a single-screw (single screw) pump, and the drive motors of this single-screw (single screw) pump is connected with a frequency converter.
3. aerated stirring foam device according to claim 1, it is characterized in that: the gas transfer pipeline between pressure regulation filter and the voltage stabilization and current stabilization metering device is provided with pressure sensor, gas transfer pipeline between voltage stabilization and current stabilization metering device and the pre-mixing apparatus is provided with another pressure sensor, this two pressure sensor all is connected with the signal input part of a controller, and the signal output part of this controller is connected with the voltage stabilization and current stabilization metering device.
4. aerated stirring foam device according to claim 2, it is characterized in that: described frequency converter is connected with controller.
5. according to claim 1 or 3 described aerated stirring foam devices, it is characterized in that: described pre-mixing apparatus by tubular shell and inner institute radially the stratiform stainless steel porous plate filler of installation constitute, end at tubular shell is shaped on gas feed and slurry import, is shaped on the compound outlet at the other end of tubular shell.
6. aerated stirring foam device according to claim 2 is characterized in that: be connected the clean water pipeline by valve between single-screw (single screw) pump and pre-mixing apparatus.
7. aerated stirring foam device according to claim 1 is characterized in that: the grout outlet at the high shear mixing emulsifier unit is connected and installed the pulp pipeline, and a magnetic valve is installed on the pulp pipeline, and this magnetic valve is controlled by a time relay.
8. aerated stirring foam device according to claim 7, it is characterized in that: the sizing head is installed in the end of pulp pipeline, this sizing head is installed on the slide, and this slide is movably installed on the guide rail, and slide is moved back and forth along guide rail by drive mechanism.
9. aerated stirring foam device according to claim 7, it is characterized in that: two sizing heads are installed on described pulp pipeline, this two sizings head symmetry is installed on separately on the slide, its slide is movably installed in respectively on the guide rail, and two slides all move back and forth along guide rail separately synchronously by drive mechanism.
Priority Applications (1)
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CN2009200969556U CN201454430U (en) | 2009-06-02 | 2009-06-02 | Novel air agitation foaming device |
Applications Claiming Priority (1)
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CN2009200969556U CN201454430U (en) | 2009-06-02 | 2009-06-02 | Novel air agitation foaming device |
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CN201454430U true CN201454430U (en) | 2010-05-12 |
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CN2009200969556U Expired - Fee Related CN201454430U (en) | 2009-06-02 | 2009-06-02 | Novel air agitation foaming device |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102318653A (en) * | 2011-06-01 | 2012-01-18 | 吴仲彬 | Automatic cake foam maker |
CN104069765A (en) * | 2014-06-27 | 2014-10-01 | 浙江圣诺盟顾家海绵有限公司 | Full-automatic foaming machine |
CN107415126A (en) * | 2017-05-19 | 2017-12-01 | 嘉善双杰海绵有限公司 | A kind of continous way sponge foaming device |
CN108497954A (en) * | 2018-04-16 | 2018-09-07 | 安捷睿(厦门)机器人有限公司 | A kind of parametrization dismisses system and liquid transporting apparatus and air transporting arrangement in real time |
CN109130055A (en) * | 2018-08-30 | 2019-01-04 | 苏州科易特自动化科技有限公司 | A kind of full-automatic emulsion foaming machine and its control system |
CN109748353A (en) * | 2019-02-22 | 2019-05-14 | 东北师范大学 | The device and method for treating water of water process are carried out based on flow control microvesicle-ozone coupling |
CN110353071A (en) * | 2019-08-22 | 2019-10-22 | 湖南元晟食品贸易有限公司 | Pre-mixing apparatus and inflator |
-
2009
- 2009-06-02 CN CN2009200969556U patent/CN201454430U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102318653A (en) * | 2011-06-01 | 2012-01-18 | 吴仲彬 | Automatic cake foam maker |
CN102318653B (en) * | 2011-06-01 | 2014-01-08 | 吴仲彬 | Automatic cake foam maker |
CN104069765A (en) * | 2014-06-27 | 2014-10-01 | 浙江圣诺盟顾家海绵有限公司 | Full-automatic foaming machine |
CN104069765B (en) * | 2014-06-27 | 2016-02-24 | 浙江圣诺盟顾家海绵有限公司 | Full-automatic foaming machine |
CN107415126A (en) * | 2017-05-19 | 2017-12-01 | 嘉善双杰海绵有限公司 | A kind of continous way sponge foaming device |
CN108497954A (en) * | 2018-04-16 | 2018-09-07 | 安捷睿(厦门)机器人有限公司 | A kind of parametrization dismisses system and liquid transporting apparatus and air transporting arrangement in real time |
CN109130055A (en) * | 2018-08-30 | 2019-01-04 | 苏州科易特自动化科技有限公司 | A kind of full-automatic emulsion foaming machine and its control system |
CN109748353A (en) * | 2019-02-22 | 2019-05-14 | 东北师范大学 | The device and method for treating water of water process are carried out based on flow control microvesicle-ozone coupling |
CN110353071A (en) * | 2019-08-22 | 2019-10-22 | 湖南元晟食品贸易有限公司 | Pre-mixing apparatus and inflator |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100512 Termination date: 20110602 |